Method of producing acicular metal crystal

ABSTRACT

Improved processes and products based on the discovery that metal atoms in complex relationship with complexing agents can be used to moderate the formation of organic salt seed crystals which promote an exceptionally well-ordered acicular growth of organometallic salts such as oxalates of the metal. Some acicular, i.e. needle-like, products have particular utility for being reduced to ferromagnetic metal particles which retain a surprisingly large degree of acicularity and possess extraordinarily favorable properties for use in magnetic recording applications.

This is a Division of application Ser. No. 401,636, filed Sept. 28, 1973now U.S. Pat. No. 3,909,240.

BACKGROUND OF THE INVENTION

During recent years, there has been a great deal of research anddevelopment activity directed to making small metallic particles,especially small ferromagnetic metallic particles for use in magnetictapes and the like. It will be understood that many of the processingimprovements developed during work on magnetic particles will also havean advantage in making non-magnetic metal particles. This is generallytrue to the extent that such parameters as uniform particle size,optimum particle size, a discrete predictable shape, favorable bulkdensity or surface area, and other such desirable physical propertiesare advantageous in metallurgical compounding work, in making catalysts,etc. Also, the reproducible, highly ordered morphology of particlesproduced by the process of the invention is believed to be of generalimportance. Thus, although the basic inventions described herein wereinitially reduced to practice during work directed towards makingimproved magnetic powders, the emphasis on magnetic particles (and theextraordinary properties thereof) in this application should not beinterpreted as an intent to waive coverage on other novel powders or onthe novel organometallic salt precursors prepared according to theinstantly-disclosed process and from which non-magnetic powders can beprepared.

Considerable emphasis on making high performance magnetic powders hasfocused, over the last ten or fifteen years, on making high-performancecobalt-based metal particles. There are a number of properties suchparticles should have and they include the following:

High Coercivity and, preferably, the temperature dependence on thecoercivity value should be minimized.

High Sigma Value--usually denotes high metal content, i.e. a minimumamount of surface oxide contamination or minimal use of non-magnetic,coercivity-inducing additives into the crystalline structure.

High Squareness--the squareness of the hysteresis loop should bemaximized. Unless otherwise noted, this squareness is measured in afield of 2000 oersteds.

Reasonable particle size--very small acicular particles, say, thosehaving an average length of as low as 0.05 microns will have enormouslylarge surface areas and will be difficult to disperse in desirablepolymeric binder media to form coatings required in manufacture ofmagnetic tape. (On the other hand, for many purposes, it is well to beable to control the process to achieve much smaller particles.)

High Acicularity--needle-like metal particles have been difficult toproduce. Even when highly acicular organometallic salts are used, theresulting metal is usually less acicular than is desired.

Good Particle Size Distribution--the above-mentioned average particlesize will have little value if the particulate product comprises anexcessive surface area due to many very small particles. (On the otherhand, larger than average particles may cause problems in metallurgicalwork.) Moreover, a relatively narrow particle size range is believed, onthe basis of work described herein, to provide favorable magneticproperties such as an excellent switching--field distribution andavoidance of bothersome D.C. saturation noise effects in magnetic memoryprocesses such as those utilizing magnetic tapes.

Stability over a period of time--earlier work has resulted in makingparticles that degraded with respect to magnetic and chemical propertiesin an undesirably short time.

Other parameters will be discussed in the body of this application.

There have been many attempts to produce improved magnetic metallicparticles for incorporation into magnetic coatings. Many of them haveinvolved the decomposition of metal carbonyl or other covalently-bondedcompounds. For example, see U.S. Pat. Nos. 3,228,882 and 3,228,881 toHarle et al and Thomas, respectively.

Other such processes have involved the use of borohydrides as reducingagents for metal ions in solution and the subsequent precipitation ofthe metal powder. Such borohydride type processes are disclosed in suchpatents as U.S. Pat. Nos. 3,206,338 to Miller et al and 3,661,556 toJolley et al.

More promising work appears to be the formation and reduction oforganometallic salts of carboxylic acids such as metal oxalates and thelike. Some such work is described in such U.S. Pat. Nos. 3,186,829 toLandgraf, 3,574,683 to Johnston, and 3,317,574 to Morita et al. The mostpertinent of this work appears in the commonly-owned and co-pendingapplication U.S. Ser. No. 228,387 filed on Feb. 22, 1972 by Ehrreich andReti now U.S. Pat. No. 3,892,673. In this work, the use of a resinouscoating envelope over the particles during reduction of an oxalate saltdid result in a product having an excellent combination of squareness,coercivity and sigma value.

However, even the powder products produced by the Ehrreich-Reti processhave limited commercial utility because of problems associated withstability of sigma value under relatively high humidity and temperature.These powder materials, when incorporated into magnetic tape, alsotended to produce a "noise" about certain narrow wavelengths and, as aconsequence, was not desirable for some magnetic tape applications.

It will be evident that the discoveries disclosed herein will beapplicable generally to the work of those who have produced powders fromorganometallic salt particles. That process is characterized by athermal step wherein the organic component of the salt decomposesdirectly to gaseous by-products leaving a metallic powder residuebehind.

Although it had been known to reduce organometallic salts such asoxalates and the like in a thermal reactor for the purpose of obtainingmetal particles, the primary concern had been to avoid such hightemperatures as will result in excessive sintering of the particle andchemical reactions which will produce excessive oxide content in thefinished particle. Thus, for example, control of sintering is one objectof the process for coating metal-bearing organometallic particles withan inert material before and during reduction to the metal powder. Thatprocess is described in a commonly-owned and co-pending patentapplication Ser. No. 367,461 filed on June 6, 1973, by Ehrreich and Retinow U.S. Pat. No. 3,843,349. That process is particularly advantageousbecause it results in particles having surprisingly desirable magneticproperties. In any event, the aforesaid discovery by Ehrreich and Retithat materials coated with resins could result in markedly improvedmagnetic properties stimulated further work in the development ofimproved processes with the general intent of further optimizing thepotential magnetic properties, especially with respect to highacicularity, freeness from DC noise manifestation when incorporated inmagnetic tape.

In a hindsight review of fields of art which have some relationship tothe invention, the following art has been uncovered:

U.S. Pat. No. 3,046,158 discloses the use of acicular seed crystals ofiron oxide which seeds are subsequently used as growth sites forproduction of acicular iron oxide. Two aspects of this patent areparticularly noted: the growth upon the seed in no way contributes toacicularity. All acicularity is contributed by the seed itself; futuregrowth in no way accentuates or preserves the acicular characterindependently of the pre-existing acicular nature of Fukada's seed.Secondly, the material being grown on the seed is the magnetic powder,not a non-magnetic precursor thereof comprising only a minor volume ofmetal.

U.S. Pat. No. 2,558,304 discusses the use of "crystal growth directors"which form complexes with hydrated iron oxide. The growth directors wereused during oxidation of ferrous compounds to make iron oxide pigmentsfor use in paint and the like.

In The Physics of Magnetic Recording by C. D. Mee (North HollandPublishing Company, Amsterdam, 1968), it is disclosed that certainacicular magnetic particles were made by Luborsky (at pages 196-198).This epic attempt to provide magnetic particles of ideal properties wasthwarted by the necessity of using special techniques which inherentlyresulted in low sigma values of the products.

U.S. Pat. No. 3,740,266 describes broad range of acicular metalparticles; applicants know of no practical way to produce acicular metalparticles from most of the alloys described therein. Most of thespecific art cited involve use of large quantities of non-ferromagneticdopes, e.g. 10-40 mole percent of Mn, Zn, Sn, Cu or Pb; or use ofalkaline earth metals or use of very small quantities of cobalt.

Other art which, when superficially examined, seems to relate to theproduct aspect of the invention is the U.S. Pat. No. 3,228,882 to Harleet al. This discloses highly acicular structure but the structure is notformed of acicular metal particles. It is formed of very small, nearlyspherical, metal particles which are incorporated in--and separatedby--an acicular matrix of resin. Such particles have a very low sigmavalue (on a volume basis) and cannot be loaded into magnetic tapeformulation in suitable quantity.

U.S. Pat. No. 3,661,556 to Jolley et al shows complexing agents in anaqueous medium in which metal powder product is formed by reduction ofmetal salts such as borohydride salts. Jolley et al disclaim knowledgeof how their mechanism works, but suggest it works by preventing theprecipitation of ferric oxide during the formation of the metal. Thatinvention teaches nothing about the utility of similar compounds in theformation of an organometallic salt which is to be collected as a solidand only later is used as a precursor to metal formed by ahigh-temperature reduction process; i.e. that invention teaches nothingabout a process of the type to be described below. Moreover, there areinherent problems associated with the Jolley et al process: e.g. lack ofhigh squareness, even when there is substantial accularity, andrelatively high non-magnetic-metal content, which prevent the productsthereof from having the unusually excellent and novel magneticproperties of the powders of the invention which will be describedbelow.

SUMMARY OF THE INVENTION

It is a principal object of the invention to provide an improved processfor making metal powders with a high degree of control over themorphology of the powders and for making novel organometallic saltprecursors of such powders.

It is a further object of the invention to provide improved metalpowders, especially improved ferromagnetic powders for use in magneticapplications.

Another object of the invention is to provide improvedmagnetic-information storing articles such as magnetic tapes and thelike.

Another object of the invention is to make small, novel organometallicsalt particles of a more advantageous shape and advantageously-orderedarrangement of atoms.

Still another object of the invention is to provide a means for avoidingthe use of resin-type encapsulating materials during reduction ofmetallic salts to metallic powders.

Another object of the invention is to provide a means for minimizing thecost of providing acicular organometallic crystals and products producedtherefrom.

It is a further object of the invention to provide an improved processfor making catalytic metal compositions and the improved compositionsthemselves and processes utilizing these compositions.

Other objects of the invention will be obvious to those skilled in theart on reading the instant application.

The above objects have been substantially achieved by utilizing thediscovery that it is advantageous to prepare highly acicularorganometallic salts from organic acids and a metal cation by initiatingthe precipitation or growth of the salt in the presence of a quantity ofcomplexing agent. The resulting metal complex (or metal complexes)apparently controls (by some directing phenomena, which may involve rateor stereochemical phenomena) the morphology and shape assumed by theembryonic and growing organometallic salts. The method is especiallyadvantageous when used to promote the growth of highly acicular salts.

One frequently-noted visual feature of the aciclic organometallic saltsprecipitated by the process of the invention is the pearlescence oriridescence of the precipitate as it forms with stirring. Moreover, adistinct pinkish color seems to predominate in cobalt-based salt systemswhereas in the prior art such systems tended to exhibit a brownishtinge. It is believed these visual features are primarily due to theuniformity of the organometallic salt's particle size and the acicularnature of the particles.

Indeed, when used to produce acicular organometallic salts such asoxalates comprising a major portion of cobalt in the metal portionthereof, it has been found that the crystalline arrangement of the saltprovides, upon suitable reduction to the metal, very substantialimprovements in the magnetic properties of the metal. Surprisingly, thehighly acicular properties of the initial precipitate (which we may calla seed) are transmitted to the organometallic salt grown from the seedand also to the metallic powder reduced from this organometallic salt.This appears in the first instance at least, due to growth of afasces-like organometallic salt which can "splinter" on reduction. Theimprovements in ferromagnetic metal powders include extremely highsquareness ratio of the hysteresis loop, and low DC noise, and highmagnetic output from tapes produced therefrom. Such metal particles,when compared to their counterparts formed by the most favorable priorart procedures, also exhibit improved chemical stability; improvedswitching fields characteristics; improved coercive force, sigma valueand squareness as a combination of properties; and an importantimprovement in the temperature dependence of the coercive force. Thelatter improvement is believed to be caused by the relative dominance ofshape anisotropy over crystalline anisotropy.

In one embodiment of the invention, the initial precipitation of seedcrystals takes place in the same medium in which the primary growth oforganometallic salt is to occur. In such a situation, it is usuallydesirable to utilize a liquid medium wherein the solubility of theorganometallic salt is less than its solubility in water. This isconveniently achieved by adding an organic solvent to the water. Suchwater-soluble solvents as acetone, lower alkyl alcohols like ethanol,and the like, are entirely satisfactory, and those skilled in the artcan select many other such readily-available solvents for use if theywish to do so.

In another embodiment of the invention, seed crystals may be formed in afirst medium containing the complexing agent and, advantageously, awater-solvent medium and then transferred to the primary crystal-growingsolution. One advantage of this latter procedure is that, when thecomplexing agent is properly selected, the population density of seedsor seed-promoting complexes in the first medium can be so high that avery small volume of the medium containing the seeds or seed-promotingcomplex can be used to initiate the growth of crystals in the primarycrystal-growing solution. This is true even when the medium for theprimary crystal-growing step is entirely aqueous. Thus, it is seen thatthis embodiment of the invention can be carried out using a relativelysmall amount of organic solvent and complexing agent.

It is possible, of course, for the complexing agent to act as asolubility-limiting material also. Indeed ethylene glycol isillustrative of one compound that is advantageously utilized in such adual role.

The term complexing agent herein is used to cover chemical compoundswhich associate with metal ions in the reaction solution. Cobalt'stendency to form such associations is well known. The association may bevia coordinate bonds, hydrogen bonds, or other such forces; theresulting compound may be looked at as a coordination complex, a chelateor more particularly described by some other terminology. Among theuseful complexing agents are organic compounds such as polyhydroxycompounds including sugars, hydroxy carboxylic acids, dicarboxylicacids, and the like. The amino and hydroxy carboxylic acidsadvantageously have an amine or hydroxyl group adjacent the carboxygroup. Inorganic compounds can also be used. Those bearing the ammoniumion are easily utilized in suitable complex formation. For the purposesof the invention the particular metal complex should at least partly bedissociable in the reaction medium. There would be no point inpermanently sequestering the metal to prevent its mobility to theembryonic seed crystal, nor would there be any point in dropping themetal out of solution in an insoluble complex precipitate. On the otherhand, if the complex is so readily dissociable in the particular mediumin which it is used that only an inoperable complex is existant, thenthe complexing agent or the medium must be changed to make thecomplexing agent useful. These considerations will be obvious tochemists reading this disclosure. However, they are made explicit herebecause of the physical impossibility of listing all of the solventsystems and complexing agents which could find use in the process of theinvention.

Among complexing agents advantageously used in the invention areincluded such compounds as sugars, especially sugars like glucose,sucrose and the like; glycols such as ethylene glycol and the like;glycerine and the like. Dicarboxylic acid complexing agents, e.g.phthalic acid and the like, are also useful. Indeed, some of the moreadvantageous aliphatic complexing agents are such aliphatic acids astartaric acid, citric acid and the like. Other such acids includeglycolic, hydroxy lactones such as ascorbic acid, lactic,hydroxy-butyric, mandelic, glyceric, malic, and the like. Ethyl alphahydroxy butyrate is believed to be another effective complexing agent asis ethylene diaminetetracetic acid. In general, the more advantageousorganic complexing agents appear to be those with two or more hydroxygroups, two or more amino groups, a hydroxy group with an adjacentcarboxyl group or an amino group with an adjacent carboxyl group. Butother such sites can interact with a cobalt ion to form a complex as isknown in the art. Using the above teachings, and the vast amount ofpre-existing literature already known to the art and which relates tocobalt-complexing agents, it is expected all skilled in the art will beable to select many additional complexing agents; all such materials,including such sometimes "chelating" agents as diethylene triamine, andthe like are intended to be covered by the term "complexing agent" asused in this application.

In many embodiments of the invention, the use of complexes seems toresult in a catalytic-like effect whereby reactions are promoted whichdo not take place, or take place relatively poorly, in the absence ofthe complex-promoted growth of seed crystals.

The cobalt-bearing organometallic salts formed of carboxylic acids bythe aforesaid complex-utilizing seeding procedure are characterized bygreat acicularity. They tend to form in what appears to be elongatefasces which, on reduction to the metal, tend to splinter along thedirection of the axis of the fasces and form elemental cobalt metalparticles of a more highly acicular and ordered crystalline structurethan has been achieved heretofore. Most important, it appears that thisacicularity of shape also manifests itself in an improved dominance ofshape anisotropy or crystalline anisotropy characteristics in magneticbehavior of the particles.

Anisotropy is the non uniformity, or directional dependence, of themagnetic properties. It is anisotropy that gives rise to the coerciveforce. Anisotropy can be caused by many different factors. In the kindof magnetic particles described herein, the dominant anisotropy factorsare shape anisotropy and crystalline anisotropy. Shape anisotropy arisesfrom the particle being unequal in length and diameter. Particles withhigh shape anisotropy are desirable because they can be oriented in amagnetic tape system and because their magnetic properties are notsubstantially influenced by changes in temperature. Crystallineanisotropy relates to anisotropies in the crystalline structure of themagnetic particle. The coercive force of a particle which derives itsmagnetic properties from crystalline anisotropy will change as about the10th power of the absolute temperature. Thus, the crystalline anisotropycan be distinguished from shape anisotropy by measuring the coerciveforce at room temperature and at some reduced temperature. Measurementsmade at about 25° C. and at liquid nitrogen temperature reveal theproducts of the instant invention and have unusually stable magneticproperties over a broad range of temperatures.

Oxalic salts are the preferred salts for use in making cobalt-bearingmetals of the invention. They tend to give the cleanest reduction stepbecause of the stoichiometric balance of the cobalt oxalate moleculewhereby the non-metallic reaction products of the oxalate are entirelygaseous. However, the process of the invention can also be carried outusing such low molecular weight carboxylate salts as formates,succinates, acetates, malonates, maleates, and the lower alkylderivatives of such compounds.

The metal component of the organometallic salt is advantageously derivedfrom such organo radicals as those normally associated with weak acids,i.e. acids weaker than the acid formed with water by the organocomponent of the organometallic salt being synthesized. These includesuch compounds as formic acid, acetic acid, and other such acids knownto the art. It should be realized that the use of such metal salts ofweak acids is not mandatory. Any increased cost in materials and processcan be measured against the value of the improved magnetic properties inany application. It is to be emphasized that inorganic salts, e.g.cobalt nitrate, are also suitable.

The advantage in magnetic properties, formed by reduction oforganometallic particles so formed, seems primarily to manifest itselfin the advantageous squareness. This is not to demean the other noveladvantages of the particles formed by the invention; but only toemphasize that squareness of 0.60 and higher, which have been extremelyelusive in formation of truly acicular cobalt-based metal particles,appear to be directly related to the crystalline order in which theorganometallic salts are formed prior to the reduction step.

A particle described herein as "cobalt-based" or "predominantly cobalt"means a particle having over 50% cobalt by weight.

It should also be emphasized that the "high" proportion of unusuallyacicular metal particles in the mass of particulate product, i.e.acicular predominantly cobalt particles having length to width ratiosfrom about 3:1 and advantageously from 10:1 to 20:1 and above haveapparently contributed a still further increase in the dominance ofshape anisotropy over crystalline anisotropy. This attribute of theinvention, in effect, can be utilized to make the coercivity of themetal powder product substantially temperature independent, i.e.coercivity change of less than 100% between -196° C. and 20° C. Indeed,this change in coercivity can be kept below 40% and even below 20% bythe process of the invention. These low increases in coercivity withtemperature are believed to be novel for predominantly cobalt particlesof the type described.

Even more important, it has been discovered for the first time thatacicular metal particles containing substantial quantities of nickel canbe made by the process of the invention, e.g. by using a cobalt oxalateseed crystal in growing a cobalt-nickel oxalate and then reducing it.For example, it is not believed that any highly acicular metal particle,i.e. having a length-to width ratio of 3:1 or better, and containing asmuch as 8% nickel has ever been manufactured in a form having desirableferromagnetic properties. But, by the process of this invention nickel,in quantities of from 8 to about 30% by weight, can be incorporated intoacicular cobalt-based particles having length-to-width ratios of up to20 - 1.

Heretofore it has not been possible to make cobalt-based magneticparticles having squarenesses as high as 0.72, achieve magneticcoercivities over 500 oersteds and volumetric sigma values over about900 emu per cubic centimeter while achieving the shape anisotropy andsize characteristics advantageous in magnetic tapes and likeapplications. Indeed, squareness values of about 0.7 to 0.88 have beenachieved, with particles formed of 50% and more of cobalt metal, by theprocess of the invention.

Another important aspect of the invention is that it provides, in someof its embodiments, a means to avoid the use of the coatings taught byEhrreich and Reti in U.S. Ser. No. 228,387, but yet achieve excellentmagnetic properties.

However, if one wishes to obtain the maximum sigma obtainable using sucha coating-free process, it may be necessary to sacrifice squareness andsome of the higher coercive force that can be achieved using thepreferred coating procedure.

A particularly interesting aspect of the above process and productsproduced thereby is that proper conditions are selected so thatextremely small organometallic crystals are formed. A very small volumeof such crystals, suitably handled and utilized in the medium in whichthey were formed, can be used to seed the growth of other suitablyacicular and suitably-sized crystals of organometallic salt. Theparticular value of this phenomenon is that the seed crystal,precipitated with the complexing agent and in a low-solubility mediumsuch as formed by ethanol and water, is effective to initiate growth ofthe greater mass of oxalate in an aqueous medium containing little or nosolubility-modifying solvent for reducing the solubility of theorganometallic salt. Thus, utilization of this seeding step markedlyreduces time, and cost and markedly increases the convenience of theorganometallic salt manufacturing operation. It is advantageous, whenforming a seed crystal by pouring a metal-bearing solution into acarboxylate-bearing solution to have some complexing agent, say a sugar,in each solution. It is also advantageous to have a solvent such asalcohol in each solution. Usually, the "seed-causing" complexing agentis carried in the metal-bearing solution.

In general, the complexing agents that are most useful in this seedingtechnique are those that permit the making of seed crystals of anextremely small particle size. Some of these complexing agents arecitric acid, hexamethylenetetramine, tartaric acid, ascorbic acid, andammonium nitrate. Others include ethylene diamine tetramine, tartaricacid, maleic acid, and alanine.

One way of evaluating a complexing agent for use in seed-type processesis to measure the viscosity of a seed material produced thereby. Ascreening test made with a Brookfield Synchroelectric Viscometer ModelRVF at a speed setting of 4, and No. 2 spindle (a No. 3 spindle may beused for the more viscous materials) has proved helpful.

The spindle is allowed to run for 60 seconds at speed before the readingwas taken. In general, it is believed that materials which yield areading below 5 are much less likely to be advantageous for use as seedmaterials than those which yield a reading above 5.

The temperatures at which the organometallic salt precipitations of theinvention can be carried out vary widely but usually will be mostconvenient between 0° F. to 200° F. The optimum temperature, like theoptimum solvent system, will usually depend on the solubility andstability of the complex itself. With most complexing agents it seemsdesirable to operate at lower rather than higher temperatures, forexample temperatures closer to 10° to 50° F. are usually better thanbetween 100°-140° F. It is not certain whether the advantage is due tothe improved complexing action at lower temperatures or to changes insolubility.

There have been no significant disadvantages experienced with thisseeding technique as opposed to the direct, i.e. one-medium process.

It should be understood, by those skilled in the art on reading thisdisclosure, that the required complexes can, in addition to being formedin place by bringing the metal cation and complexing agent together in asolution, be formed by bringing a solid reaction product comprising themetal cation and complexing agent into the solution wherein theorganometallic salt is to be formed. For example, a solid product ofcobalt and citric acid is a suitable solid precursor for solublecomplexes which are useful in the process of the invention. The citricacid radical apparently provides, in solution with cobalt, the requiredcomplexing agent or agents.

The mechanism by which the process of the invention operates does notseem to be explained by reference to conventional seeding technology. By"operation" in this paragraph is meant operation in the chemical processsense; no reference to the extraordinary magnetic properties and theunobviousness of using the disclosed process to obtain them isintended). It may be that the complexing agents used form a plurality ofspecies of complexes with the selected complexing agents, that thesedifferent complexes have different solubilities, that some of them tendto initiate crystal growth while others tend to moderate the rate orextent of growth once it is initiated. In any event, patentability ofthe invention herein is not predicated on an understanding of theprecise physicc-chemical mechanism of the reactions involved therein.

In general, the kinds of agents used by Jolley et al and described inColumns 2 and 3 of U.S. Pat. No. 3,661,556 are useful with the processof this invention when utilized with properly balanced solvent medium.That disclosure is incorporated by reference in this specification.Martel and Calvin, in "Chemistry of the Metal Chelate Compounds",(Prentice-Hall, Incorporated, New York, New York, 1950, ppg. 514-558)also provide useful information for those who wish to use complexingagents other than those specifically described herein. Nothing in thisparagraph should be construed to imply that the function of the"chelating agents" of Jolley et al is the same as the complexing agentof the instant invention. The term "chelate" connotes a capture ofundesirable species and Jolley et al believe their metal-forming processworks that way. Applicants believe that the complexing agents of theirinvention have a positive effort on promoting the favorable crystalgrowth of their organometallic salts; although, of course, the actualmechanism by which such beneficial results are achieved remain unknown.

In the drawings:

FIGS. 1 through 3 show typical hysteresis curves of a novel magneticpowder produced by the process of the invention as described in Example19. FIG. 1 is an integrated hysteresis loop; FIG. 2 is a similar loopbut with an unintegrated value of the magnetic moment with time (a dM/dtcurve); and FIG. 3 shows a series of hysteresis loops achieved for asingle sample of particles under varying applied magnetic fields.

FIGS. 4 and 5 are similar to 2 and 3 but are descriptive examples ofsamples representative of applicants' best efforts before the making ofthe present invention.

FIGS. 6 and 7 are similar to 4 and 5 but represent 85 cobalt-15% nickelparticles of the above-mentioned Ehrreich-Reti invention, the best knownprior art in the statutory sense. The abscissa of the graphs of FIGS. 1,3, 4 and 6 ranges from -2000 to +2000 oersteds and represents the 2000oersted magnetic field in which the measurements are carried out. Theordinate can be considered as arbitrarily selected to aid demonstrationof the difference between tested specimens. (The abscissa in FIGS. 2, 5and 7 is reversed, and reads from +2000 to -2000, left to right.)

The drawings must be interpreted with the following in mind: they are inmany respects comparative, measured on the same BH meter andconsequently characteristics attributable to the electricalcharacteristics of the meter are a common factor in all the drawings. Ingeneral, this is a minor factor. Most useful BH meters will produce verysimilar curves. Moreover, in making such pictures, as shown in FIGS. 2,5 and 7, the distance from the origin (zero field point) to the peaksshould be not more than about one-third of the distance from the originto the maximum applied field. This is to assure that a particularangular function tending to "fatten" these peaks is made negligible.

However, once these facts are realized, the drawings in FIG. 2, 5 and 7can be used to define highly advantageous and novel features of theinvention.

ΔH, peak-spread width at 50% of the peak height, over H, the distancefrom origin of the curve to the vertical line from the center of thepeak. It is believed that acicular based particulate material known tothe prior art has ever had a value of ΔH/H of less than about 0.75. Yetthe value of the material of Example 19 is about 0.62. Similarimprovements are generally assignable to acicular products of theinvention.

Making Magnetic Tape

The metal powders produced by the processes of this invention may beadvantageously incorporated into magnetic tape utilizing many differentpolymer systems. However, in order to obtain a favorable loading it isbelieved to be most desirable to use pre-polymerized urethane resinsystems. One such system would comprise 77 parts by weight of the metalpowder product of Example 9, 2 parts soya lecithin, 19 pounds of thepre-polymerized polyurethane resin sold under the trade designationEstane 5707 by B. F. Goodrich Co., and as described in U.S. Pat. No.2,871,218 to Schollenberger. Other additives would normally be added.These additives are known to those generally skilled in the art, andinclude fungicides, and the like. Two parts by weight of butoxyethylstearate and 0.1 part by weight of diphenyl mercury would be suitableadjuvants for the formulation given above. The formulation whenadequately mixed would be coated along a substrate such as apolyethylene terephthalate polymer film substrate, dried and slit forwinding onto spools: all such processes are well known in the art.

Although the advantages of the ferromagnetic powders manufacturedaccording to the invention can be achieved without supplementaltreatment or compounding,, it is noted that there will be someapplications wherein formation of a suitable magnetic tape product willmake it advantageous to add certain other magnetic powder thereto, e.g.ferromagnetic metal oxide powders or doped metal oxide powders to act asdispersing aids. Nevertheless, one advantage of the invention disclosedherein is that one may substantially avoid use of additives whichcontain non-ferromagnetic atoms (which usually either increase thecrystalline anisotropy, decrease the magnetic moment or interfere withthe chemical stability of the resulting particulate mass) and stillachieve a recording medium of extraordinary quality.

Distribution of Switching Fields

A particularly advantageous feature of the invention is the ability toavoid unwanted magnetic switching in the magnetic fields of relativelysmall magnitude, i.e. in fields of from 0 to 200 oersteds. In a typicalsample, there may be an absence of any significant switching below 200oersteds, then be a significant amount of switching by the time thefield is increased to 250 oersteds, and--finally--90% of the particleswill switch when the field reaches the 500-oersted level.

This distribution of switching fields may differ somewhat as theformulation of morphology of particular products differs but theprinciple discussed in this paragraph relates in general to thefavorable attribute of those particles of the invention which lack anysignificant switching over at a higher field. This feature makes theparticles suitable for use in some magnetic memory applications wherein,say, very little switching is desirable at one field and the switchingtakes place with an increased field. This attribute is particularlyimportant in avoiding print-through in reeled magnetic tape.

Another interesting application of particles having this advantageousswitching characteristic is current-limiting transformer. For example, atransformer core would consist of particles of the type being discussed.The primary winding would be in an electrical circuit. As current ischanged in the circuit, there would be no response to the presence ofthe core material as long as the current was not such as to induce afield of, say, 200 oersteds. However, when the current rises above apre-selected value (determined by the number of windings of dimensionsof the core) the field would exceed 200 oersteds and, at this point, theparticles would begin to switch. It is only when this switching beginsthat the transformer makes its "appearance" in the circuit. Thetransformer would be fully operable by the time the field strengthreached 500 oersteds. The secondary windings of the transformer could goto a resistive element which could serve to dissipate energy. On theother hand, a secondary element might consist of a feedback route tomoderate the signal in the primary electronic circuit. A thirdpossibility would be to have the secondary windings connected to analarm bell or other such signal device.

Such a current-limiting transformer has a great many applications. Itcould be used to limit current and would have advantages over thefuse-type devices used today. Fuse-type devices shut down apparatus, ineffect destroying the circuits.

FIG. 3 discloses a series of hysteresis loops of one such material (thatdescribed in Example 18), a cobalt-based particulate material, whichwould be incorporated into such a core for use in the transformerdescribed above. The central diagonal line was taken at 200 oerstedsapplied field. The smaller loop around the diagonal line was measured ata field of 250 oersteds, then, reading out from the center, the nextsequential loops were measured at 500, 750, and 1000 oersteds appliedmagnetic fields.

The distribution of switching fields plots the histogram of the numberof particles which begin switching in a given increment of appliedfield. The coercive force of the group of particles is a measure of aweighted average of where the particles switch, but coercivity does notprovide any information as to how the data is distributed around theaverage value. The histogram of FIG. 3 presents this distribution data.For magnetic recording use, the distribution of switching fields need tobe sharply distributed. A broad distribution causes severe problems inthe design of the recording head and in the design of equalizationelectronics.

Another advantageous property of the process and novel powders producedthereby is the ability to provide powders having the extraordinarilyfavorable magnetic properties, mentioned elsewhere in thisspecification, and also exhibiting an extremely favorable dM/dt curve.This curve (as indicated in FIG. 2) exhibits the unintegrated value ofthe magnetic moment (M) as a function of time. It is distinguished fromthe hysteresis loop of FIGS. 1, 4 and 6 in that the hysteresis loop ofthese curves represents the integrated value of M. For manyapplications, a dM/dt curve that is sharply peaked, as opposed to acurve that is more gradually peaked, is thought to be particularlydesirable. For example, in high-frequency magnetic recording, a curvewhich peaks and drops sharply and approaches its terminal points in anearly horizontal direction is favored.

In this specification, the particular advantage of the claimed processeswill often be most clearly identified by the magnetic properties ofpowders produced thereby. Applicants believe that such magneticproperties result from the particular order, molecular or atomic orcrystalline, which the processes allow to be imparted to the materialbeing described and to the uniform morphology of the resultant powder.However, it should be realized that even when the nature of the particleis not adequately measured by magnetic means (say, when the particle islargely non-magnetic in properties) an advantageous morphology or orderis still contributed by the processing technique. Thus, such an ordermay contribute good optical properties to a pigment, goodchemical-activity properties to a catalyst, or the necessary size, shapeand crystalline uniformity to a powder to be used in coating or alloyingprocesses.

Moreover, within the field of magnetic particles, it should be realizedthat such terms as "high squareness", "high coercivity", and the likeare not absolute, but depend upon the particular metallic morphologybeing measured. Thus, applicants' ability to achieve squareness over,say, 0.70 in cobalt-based systems and to obtain such predominant shapeanisotropy is illustrative of a general process capability of favorablycontrolling the particle size distribution and the crystalline structureof the particles being measured. This capability is new and should berecognized to have value even in systems where the results cannot be sodramatically shown to be novel as they can be in magnetic systems.

As a general proposition, it appears that crystals formed according tothe invention, i.e. formed by the use of complexing agents or by the useof seed crystals which have been formed by the use of complexing agents,can themselves serve as seed crystals for propagation of furthercrystals having many of the advantages of the initially-formed crystalproducts. Of course, as the sequence of using seed crystals insubsequent batches proceeds, the seed crystals become larger and so dothe crystal products formed therewith. But, for applications where verysmall size of the organometallic salt product is not necessary, thereare compensating advantages. For example, squareness of the metalproduced from the larger particles so produced appears to be even morefavorable than that of earlier-produced smaller particles.

Illustrative Examples of the Invention

In order to point out more fully the nature of the present invention,the following working examples are given as illustrative embodiments ofthe present process and products produced thereby.

Unless otherwise specified, the specific examples disclosed below arecarried out according to the following general procedure:

The precipitation is carried out in a 1000 ml Erlenmeyer flask with fourbaffle-type indentations molded at 90 angular degree intervals aroundthe base of the flask. Agitation is achieved by a magnetic stirring barabout 1.6 inches long and 0.5 inches in diameter.

The addition of solutions to the flask is accomplished through a funnel.The times of addition are longer as the viscosity of the solution beingadded increases.

Cobalt nitrate is used as the cobalt source but other such water-solublecobalt salts as the acetate, chloride or sulfate are generally useful.The commercial varieties of these salts normally contain 3% of nickelbased on the weight of cobalt. Experiments have indicated there islittle or no advantage to the use of pure cobalt salts.

The water is used as deionized water processed through a standardcommercial laboratory deionizer. A colorless commercial syrup is used asa source of sugar complexing agent. It is that material sold under thetrademark Karo by Best Foods of Engelwood Cliffs, New Jersey and isreferred to hereinafter as Karo. It is formed principally of the typethat digests to dextrose units. When sucrose is specified, ordinarysugar from any grocery store is used. Other reactants are utilized intheir ordinary commercial form. The methanol is Reagent Grade, but suchpurity is not required. The ethanol is denatured ethanol. The glycerineis U.S. Pharmacopeoia grade, but again this purity is probably notrequired.

The organometallic salts, the preparation of which is disclosed beloware coated with a resin and decomposed as follows:

The organometallic salt filter cake is air dried after washing andrewetted with isopropanol. A polyamide resin, sold under the trademark"Resymide 1125" by RESYN Corporation of Linden, New Jersey (andhereinafter referred to as "Resymide"), is dissolved in isopropanol. Aquantity of the resin is used which is about 7% of the weight of themetal in the organometallic compound to be coated. The isopropanolsuitably contains a concentration of about 10% resin. A thin slurry ofthe organometallic salts in the resulting liquid is formed and theisopropanol is evaporated as the slurry is stirred. The resulting drypowder is a mass of resin-coated particles ready for reduction.

In general, the reduction is carried out by placing the powder in sampleboats containing eight different compartments. (Usually a differentsample is in each compartment to facilitate comparative testing.) Thesample boats are sealed in tubes having gas inlet and gas outlet ports,then placed in an oven, with conduits to both the outlet and inlet portextending from the oven to a gas-supply source and a gas exhaust system,respectively. The tubes are purged with N₂ ; then the oven temperatureis set for 650° F. and a gas mixture of 20% hydrogen and 80% nitrogen ispassed through the tubes at the rate of 40 cc per minute. Within about45 minutes, CO₂ evolution starts. After the rate of CO₂ evolution peaksand drops to less than 0.01% by volume of the offgas, the tube is purgedwith nitrogen, and removed from the furnace. After cooling to roomtemperature--this usually takes an hour or so--a mixture of 3% oxygenand 97% nitrogen is passed through the tube. This gas mixture is usuallyallowed to run for several hours but the exact time, or even the exactcomposition, is not particularly critical.

Then the reacter is purged with air for two hours and opened. Thesamples are removed and are ready for analysis.

Usually a sample from a control batch of oxalate is fired with eacheight-sample load as a means to confirm the reproducibility of thereduction process.

EXAMPLE 1

A quantity of 25.2 grams of oxalic acid dihydrate is dissolved in amixture of 250 grams of Karo and 150 grams of water to form a firstsolution. To this first solution is added a second solution of 29.1grams of cobalt nitrate hexahydrate in 100 grams of Karo and 50 grams ofwater. This addition is made over a period of about 30 minutes.

After the addition is completed, stirring is continued for an additional30 minutes.

The mixture was filtered and washed two times with distilled water at60° C. The filter cake, beige initially, turned pinkish in color onbeing washed with the water. Next the precipitate is washed in acetone.A sample is collected for a microscopic inspection; the remainder of theprecipitate is resin coated and reduced to metal.

EXAMPLE 2

A procedure similar to that of Example 1 was followed excepting thefirst solution was comprised of 25.2 grams oxalic acid dihydrate, 200grams of sucrose and 200 grams of demineralized water. The solutionadded to the first solution, through a funnel and over a period of about13 minutes, was formed of 29.1 grams of cobalt nitrate hexahydrate in 75grams sucrose and 75 grams of water.

Samples were taken as indicated in Example 1. After the precipitation ofthe cobalt oxalate salt, it was filtered, washed and reduced to form ametal powder more fully described in Table A.

The following examples were carried out, according to the generalprocedures of Example 2, to form metallic powders. Properties of thesemetals and the organometallic salt precursor are given in Table A.

EXAMPLE 3

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        Oxalic acid              Cobalt nitrate                                       dihydrate   25.2   gm    hexahydrate                                                                              29.1 gm                                   glycerine   200    gm    glycerine  75   gm                                   water       200    gm    water      75   gm                                   ______________________________________                                    

Addition time was 6 minutes and 9 seconds.

EXAMPLE 4

    ______________________________________                                        Solution 1        Solution 2                                                  ______________________________________                                        Oxalic acid 25.2   gm     Cobalt nitrate                                                                          29.1 gm                                   dihydrate                 hexahydrate                                         ethylene glycol                                                                           200    gm     ethylene glycol                                                                         75                                        water       200    gm     water     75                                        ______________________________________                                    

Addition time was 5 minutes and 45 seconds.

EXAMPLE 5

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        Oxalic acid              Cobalt nitrate                                       dihydrate   25.2   gm    hexahydrate                                                                              29.1 gm                                   ethanol     125    gm    ethanol    50   gm                                   water       125    gm    water      50   gm                                   Karo        150    gm    Karo       50   gm                                   ______________________________________                                    

The addition took 10 minutes and 4 seconds. The mixing action wasrelatively poor because of the viscosity of the mix.

EXAMPLE 6

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        Oxalic acid              Cobalt nitrate                                       dihydrate   25.2   mg    hexahydrate                                                                              29.1 gm                                   acetone     125    gm    acetone    50   gm                                   water       125    gm    water      50   gm                                   Karo        150    gm    Karo       50   gm                                   ______________________________________                                    

Again, the addition time took about 6 minutes.

EXAMPLE 7

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        Oxalic acid              Cobalt nitrate                                       dihydrate   25.2   gm    hexahydrate                                                                              29.1 gm                                   water       375    gm    water      140  gm                                   Karo        25     gm    Karo       10   gm                                   ______________________________________                                    

Solution 2 was added to Solution 1 in a little less than 5 minutes. Theacicularity of the oxalate increased and, consequently, the bulk densitydropped.

EXAMPLE 8

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        oxalic acid              cobalt nitrate                                       dihydrate   25.2   gm    hexahydrate                                                                              29.1 gm                                   Karo        400    gm    Karo       120  gm                                   water       100    gm    water      30   gm                                   ______________________________________                                    

It took about 37 minutes to add Solution 2 to Solution1. The stirringwas sluggish because of the high viscosity.

The product had a low bulk density, and less acicularity.

EXAMPLE 9

    ______________________________________                                        Solution 1        Solution 2                                                  ______________________________________                                        oxalic acid 25.2   gm     cobalt nitrate                                                                            19.4 gm                                 dihydrate                 hexahydrate                                         isopropanol 125    gm     ferrous sulfate                                                               heptahydrate                                                                              9.3  gm                                 water       125    gm     isopropanol 50   gm                                 propylene glycol                                                                          75     gm     water       50   gm                                 ethylene glycol                                                                           75     gm     propylene glycol                                                                          25   gm                                                           ethylene glycol                                                                           25   gm                                 ______________________________________                                    

Addition time was about 6.5 minutes.

                                      TABLE A                                     __________________________________________________________________________    PROPERTIES OF POWDERS                                                         Example No.                                                                            1    2         4    5    6    7    8    9                            __________________________________________________________________________    Specific Magnetic                                                              Moment  125  117  122  118  119  114  119  110  96                           Coercive Force,                                                                Room Temp.                                                                            770  783  715  799  1020 1020 730  773  1010                         Coercive Force,                                                                Liq. N.sub.2 Temp.                                                                    1344 1480 1340 1400 1690 1848 --   --   1380                         Ratio Liq. N.sub.2 /                                                           Room Temp.                                                                            1.75 1.89 1.87 1.75 1.66 1.81 --   --   1.37                         Squareness                                                                             .78  .78  .78  .81  .79  .80  .76  .73  .63                          Particle Size                                    --                            Length, Ave                                                                           10.6 9.3  10.1 7.5  3.5  6.3  7.9  15.1 --                            Std. Dev.                                                                             4.6  4.1  2.7  3.9  1.0  1.6  3.3  9.1  --                            Width, Ave                                                                            .82  .59  .71  .41  0.20 .41  1.34 1.37 --                            Std. Dev.                                                                             .44  .36  .22  .19  .04  .07  .67  .47  --                            L/D Ratio, Ave                                                                        14.6 18.4 15.4 20.2 17.9 15.8 7.95 11.5 --                            Std. Dev.                                                                             5.8  10.5 5.6  11.4 5.0  4.9  4.6  5.4  --                            Min. Value                                                                            6.2  6.7  8.7  7.1  10.0 10.6 3.75 4.5  --                            Max. Value                                                                            29.4 54.0 27.4 55.4 33.3 29.6 14.9 24.3 --                           __________________________________________________________________________

EXAMPLE 10

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        oxalic acid              cobalt nitrate                                       dihydrate   9.8    gm    hexahydrate                                                                              14.2 gm                                   water       120    ml    nickel nitrate                                                                           2.0  gm                                                            hexahydrate                                          Karo        280    ml    water      140  ml                                                            Karo       140  ml                                   ______________________________________                                    

Solution 2 was added dropwise to Solution 1. The resultant precipitatewas filtered, washed with hot water, then isopropanol, then dried. Itwas then coated with a solution of phenoxy resin dissolved intetrahydrofuran. This resin is sold under the trademark PKHH by UnionCarbide. A quantity was used equal to 7% of the weight of the metal inthe salt. The salt was reduced according to the general procedure setforth above.

The resulting metal powder had a coercive force of 640 oersteds, asquareness of 0.76 and a magnetic moment of 109 emu per gram.

EXAMPLE 11

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        oxalic acid                                                                              25.2   gm     cobalt nitrate                                                                           29.2 gm                                                            hexahydrate                                          water      500    ml     ethylene glycol                                                                          25   ml                                                            Karo       25   ml                                                            water      50   ml                                   ______________________________________                                    

Solution 2 was added dropwise to the oxalic acid-containing solutionover a period of one hour. The precipitated cobalt oxalate was easilyfiltered, and washed as in Example 1. Before being reduced, the oxalatewas subjected to optical analysis by a scanning electron microscope. Theobserved results:

    ______________________________________                                                    Average                                                                              Max     Min     Std. Dev.                                  ______________________________________                                        Length, microns                                                                             58.5     99.9    17.1  22.8                                     Diameter, microns                                                                           2.3      3.6     1.6   0.49                                     L/D ratio     24.3     42.1    10.6  8.6                                      ______________________________________                                    

A very readily filterable oxalate with a high degree of acicularity wasobtained.

EXAMPLE 12

    ______________________________________                                        Solution 1        Solution 2                                                  ______________________________________                                        oxalic acid               cobalt acetate                                      dihydrate   25.2   gm     tetrahydrate                                                                             25  gm                                   water       335    ml     glacial acetic                                                                           1   ml                                                             acid                                                ethanol     165    ml     Karo       85  ml                                                             water      45  ml                                   ______________________________________                                    

After Solution 2 was added to Solution 1, an organometallic salt, i.e.cobalt oxalate was precipitated, washed, dried, coated and reduced ashas been described above.

The resulting magnetic cobalt particles have a coercive force of 1212oersteds, a squareness of 0.74 and a specific magnetic moment of 108.The coercive force at liquid nitrogen temperature was 1440 oersteds,showing the relatively small crystalline anisotropy effect.

EXAMPLE 13

    ______________________________________                                        Solution 1       Solution 2                                                   ______________________________________                                        oxalic acid 25.2   gm    cobalt nitrate                                                                           29.2 gm                                                            hexahydrate                                          water       400    ml    tartaric acid                                                                            30   ml                                                            water      200  ml                                   ______________________________________                                    

Solution 2 was added dropwise to Solution 1 with vigorous stirring.Acicular crystals of the resulting cobalt oxalate were formed. Thecrystals were highly permeable to liquid and were easily washed.

A sample of thirty crystals was measured by electron photomicrograph.Average length was 6.47 microns (std. deviation 2.3, range 1.7 to 10.7microns). Average width was 0.447 microns (std. deviation 0.12, range0.78 to 0.28). The average length: diameter ratio was 15.1 (std.deviation 5.98, range 47 to 28.3).

Coercivity of the mass of particles was 886, the magnetic moment was 128and a squareness of 0.803.

EXAMPLE 14

A seed crystal mixture was prepared according to the followingprocedure:

    ______________________________________                                        Solution 1        Solution 2                                                  ______________________________________                                        Cobalt acetate                                                                             25 gm    oxalic acid 25.2 gm                                                           dihydrate                                               citric acid  25 gm    dihydrate                                               water        50 gm    Karo        150  gm                                     Karo         50 gm    water       150  gm                                     ethanol      50 gm    ethanol     150  gm                                     ______________________________________                                    

Solution 2 is added slowly at 18° C. into Solution 1 in a 1 literbaffled Erlenmeyer flask equipped with a magnetic stirring bar.Initially stirring is so vigorous that bubbles of air are whipped intothe oxalic solution. When about a third of the Solution 2 is added, thematerial will be so viscous that it will no longer vortex. The agitatoris stopped momentarily to clear the solution of air bubbles, thenstirring is resumed. The cobalt is introduced about 1/8" above themagnetic stirring bar. As the remainder of the cobalt is added the mixbecomes a very viscous suspension. A 200 milliliter sample of thissuspension is filtered on a Buchner vacuum filter using Whatman #5filter paper. The crystals were washed with 400 milliliters hot waterand then with 200 milliliters acetone. The crystals lift off the filterpaper as a paper-like sheet. These crystals were difficult to photographand measure, but size data is included in Table I and is based onscanning electron microscope (SEM) pictures taken at 10,000X. A 5 gramsample of these crystals was coated with 0.113 grams of Resymide inisopropyl alcohol. The alcohol was evaporated and the powder placed in atube furnace sample boat. It was reduced in 20% hydrogen and 80%nitrogen until the CO₂ in the vent gas dropped below 0.04%. It wascooled to 20° C. under nitrogen and then exposed to 3% oxygen innitrogen for 16 hours. The sample was next exposed to dry air for twohours and then analyzed magnetically. Data is given in Table B.

EXAMPLE 15

    ______________________________________                                        Solution 1        Solution 2                                                  ______________________________________                                        cobalt nitrate            oxalic acid                                         hexahydrate  29.1   gm    dihydrate 25.2 gm                                   water        150    gm    water     250  gm                                   ______________________________________                                    

Solution 2 was made in a 1000 milliliter baffled Erlenmeyer flaskequipped with a magnetic stirrer. When the oxalate was dissolved, 2milliliters of the seed solution in Example 14 were added to Solution 2.Then Solution 1 was added slowly to the seed-bearing mixture. Abeige-pink precipitate resulted. This material was filtered, washed with600 milliliters hot water and 200 milliliters of acetone. The crystalswere sampled for SEM photographs. 10 grams of this oxalate was coatedwith 0.225 grams Resymide and reduced according to the proceduredescribed in Example 1. Data on the metal is given in Table B.

EXAMPLE 16

The experiment was identical to Example 15, except that 10 millilitersof seed mixture was added to Solution 2. Data on the metal is given inTable B.

EXAMPLE 17

The experiment was identical to Example 15, except that 50 millilitersof seed mixture was added. Data on the metal is given in Table B.

EXAMPLE 18

The experiment was identical to Example 15, except that 200 millilitersof seed mixture was added. Data on the metal is given in Table B.

                  Table B                                                         ______________________________________                                        Metals of Examples 14-18                                                                Example Number                                                                Control                                                                              14      15     16   17   18                                  ______________________________________                                        Milliliter of                                                                 Seed Added  None (All Seed)                                                                            2      10   50   200                                 Coercive Force, oe.                                                                       805      1087    758  840  823  1038                              Squareness  .75      .74     .79  .83  .82  .77                               Specific Magnetic                                                             Moment      115      106     102  120  110  121                               Length, Microns                                                                 Average   8.7      2.5     9.4  7.7  7.05 2.38                                Maximum                    16.5 20.5 10.6 4.1                                 Minimum                    3.8  1.6  4.4  1.1                                 Std. Dev  3.4              3.3  3.9  2.0  .85                               Diameter, Microns                                                               Average   1.5      .19     1.2  .75  .53  .35                                 Maximum                    1.84 1.3  .83  .45                                 Minimum                    0.49 .37  .34  .27                                 Std. Dev. .66              .38  .27  .13  .05                               L/D Ratio                                                                       Average   6.4      13.3    8.33 11.4 13.9 6.8                                 Maximum   10.0             14.8 30.8 23.3 12.2                                Minimum   2.4              3.4  2.3  7.6  3.0                                 Std. Dev. 1.8              3.0  6.9  4.4  2.5                                 N                          18   26   16   17                                ______________________________________                                    

EXAMPLE 19

A seed crystal was prepared as in Example 14. 100 milliliter of seedsuspension was placed in a baffled 1000 milliliter Erlenmeyer flask. Asolution containing 25.2 grams of oxalic acid dihydrate and 400 grams ofwater was added slowly to the seed crystals with agitation. Next asolution containing 18 grams of cobalt nitrate hexahydrate, 5 grams offerrous sulfate heptahydrate and 5 grams of nickel nitrate hexahydratein 150 grams of water was added slowly with agitation, 10 minutes beingrequired for complete addition. A pearlescent suspension results whichis light yellow in color. These crystals were filtered in a Buchnerfunnel, washed with 600 milliliters of hot water, rinsed with acetoneand dried. They were weighed, wetted with isopropanol and coated withresymide in isopropanol at a level corresponding to 7 weight % based onmetal content. The isopropanol was dried and the particles reduced in atube furnace as before. These particles had a:

Specific magnetic moment--138 emu/gram

Coercive force--659 oersteds

Squareness--0.84

Drawings of the hysteresis loop and of the dM/dT curves are shown inFIGS. 1-3. Samples of this material were stored in a humidity oven(Tenney Engineering, Union, New Jersey, Model TMTH 0200) at 66° C. and50% relative humidity for 1601/2 hours. After this exposure, thespecific magnetic moment was found to be 112 emu/gram.

The material comprises about 18% nickel, 18% iron and 64% cobalt and hasan extraordinary combination of corrosion-resistance and magneticproperties.

EXAMPLE 20

A seed crystal suspension was prepared as shown in Example 14. 100milliliters of suspension was placed in a 1000 milliliter baffledErlenmeyer flask. A solution of 25 grams of oxalic acid dihydrate in 250grams of water was added slowly while stirring. An additional 50milliliters of water was used to rinse the remaining oxalic crystalsinto the flask. A suspension of 11.8 grams of commercial cobaltcarbonate in 200 milliliters of water was added slowly, 7 minutes beingrequired. Bubbles of gas rise to the top gradually as the cobaltcarbonate is added. The mixture was allowed to stir for 30 minutes at23° C. A light pink colored precipitate is formed. 100 milliliters ofthis first suspension was set aside and the remainder was filtered,washed, rinsed with isopropanol, dried, weighed, coated with 7% resymidebased on cobalt and reduced to metal. This sample is labeled "A" in thetable of magnetic properties.

The 100 milliliters of the first suspension was mixed with 25 grams ofoxalic acid solution and then 11.8 grams of cobalt carbonate suspensionwas added. The resulting suspension of precipitate was thick, but wasmore tan in color than the previous one. 100 milliliters of this secondsuspension was also set aside and the remainder filtered, coated, andreduced to metal. This sample is labeled "B". The 100 milliliters ofsecond suspension was used as above to make a precipitate which wasreduced to metal powder "C"; a third 100 milliliter sample of suspensionwas reserved during the procedure. This precipitate was brownish incolor. 100 milliliters of the third suspension was used to make aprecipitate which was brownish in color and which was reduced to metalpowder "D". Table C shows the properties of the metals formed.

                  Table C                                                         ______________________________________                                        Metal Coercive                   Magnetic                                     Powder                                                                              Force          Squareness  Moment                                       ______________________________________                                        A        767         0.70        145                                          B        704         0.72        146                                          C        720         0.75                                                     D        711         0.77        143                                          ______________________________________                                    

EXAMPLE 21

A seed crystal was prepared as described in Example 14, but usingalanine in place of citric acid. A quantity of 100 milliliters of theresulting alanine seed crystal suspension was added to a solutioncontaining 25.2 grams of oxalic acid dihydrate and 400 milliliters ofwater. A solution of 29.1 grams cobalt nitrate hexahydrate in 200milliliters of water was added slowly to the oxalic acid seed crystalmixture. A thick pink precipitate resulted which was filtered, washedwith hot water, dried with isopropyl alcohol, weighed, coated withResymide and reduced in the tube furnace as described in Example 1. Themagnetic properties of this powder were measured to be as follows: 118emu/gram specific magnetic moment; 850 oersteds coercive force; and 0.78squareness.

EXAMPLE 22

A seed crystal was prepared as follows: a solution was prepared of 25.2grams oxalic acid dihydrate, 150 grams Karo syrup, 150 grams denaturedethyl alcohol, and 150 grams water. To this solution was added asolution containing 29 grams cobalt nitrate hexahydrate, 32 gramsammonium nitrate, 50 grams Karo, 50 grams denatured ethyl alcohol, and50 grams of water. A suspension of a very viscous pink precipitateresulted. A quantity of 100 milliliters of this suspension was added toa solution containing 25 grams of oxalic acid dihydrate and 400milliliters of water in a 1 liter, baffled Erlenmeyer flask equippedwith a magnetic stirrer. To this mixture was added a solution containing29.1 grams of cobalt nitrate hexahydrate and 200 milliliters of water. Apink precipitate resulted which was filtered, washed with hot water,washed with alcohol and dried. The sample was weighed and the usualquantity of Resymide was added in isopropyl alcohol. The resultingsolution was dried and fired in the tube furnace as described inExample 1. The magnetic properties of this material were found to be:specific magnetic moment of 126 emu/gram; coercive force of 625 oerstedsand a squareness of 0.81.

Catalysts

As has been indicated elsewhere in this specification the processes ofthe invention are useful in forming novel particles having use outsidethe magnetic applications areas. Many of these areas have very limitedtheoretical basis for explaining the exact properties which contributeto the utility. Nevertheless, applicants' experience clearly indicatesthat the ordered arrangement and uniformity of particles made possibleby their complex-agent-modified seeding process is directly responsiblefor whatever esoteric balance of properties result in the extraordinaryproperties of such materials.

One of the particular advantages of the invention is that it providesmeans to manufacture novel and improved metal catalysts which haveexcellent activity and can be duplicated with excellent predictability.

One of the well-known catalysts now used in many chemical processes isthe so-called Raney catalyst. This catalyst is expensive and is notstable. Consequently, it is usually freshly prepared each time it isused. Some investigators have claimed stability of the Raney-typecatalyst if the material is kept in a refrigerated condition and underdry alcohol. However, even under these conditions, catalytic activitywould last only a couple of days. From the foregoing it is clear that itwould be highly desirable to provide an improved, more stable and moreeffective catalyst to replace the conventional Raney-type.

EXAMPLE 23

A seed crystal was prepared by dissolving 25 grams of cobalt acetatetetrahydrate, 25 grams of citric acid, and 50 grams of the dextrosesyrup sold under the trade name Karo in 50 grams of water and 50 gramsof denatured ethanol (ethyl acetate and other alcohols were used as thedenaturants in this commercially-obtained denatured alcohol). A secondsolution was prepared containing 25.2 grams oxalic acid dihydrate, 150grams of ice, 150 grams of the aforesaid denatured ethanol, and 150grams of the aforesaid dextrose solution. The second solution was placedin a 1 liter Erlenmeyer flask equipped with a magnetic stirrer. Thefirst solution was then added slowly to the second solution whilestirring the mixture. A very thick viscous suspension of cobalt oxalateseed crystals resulted.

A quantity of 50 ml of this seed crystal suspension was placed in asecond one-liter baffled Erlenmeyer flask which contained 25 grams ofoxalic acid dihydrate dissolved in 500 ml of water.

Thereupon, a nickel-bearing solution was prepared containing 27.6 gramsof nickel nitrate hexahydrate in 150 ml of water; 100 ml of thissolution was added slowly to the contents of the second Erlenmeyerflask. Vigorous stirring was maintained throughout the addition.

The excess of the solution over and above the 100 milliliters added tothe second Erlenmeyer flask was mixed with a solution containing 1.25grams zinc nitrate and 50 milliliters of water. This mixture was thenadded to the ultimate suspension of nickel oxalate particles withagitation. Next, the suspension was filtered, washed with 500milliliters of hot water, then with 250 milliliters of acetone, and thendried. The resulting particles were reduced to metal particles byheating in a tube furnace at 650° F. while passing a mixture of 20%hydrogen and 80% nitrogen gas through the furnace until the evolution ofCO₂ stopped.

The sample was allowed to cool in the presence of a 20% hydrogen-80%nitrogen mixture for 16 hours. It was then covered with dry isopropylalcohol.

The specific magnetic moment, i.e. sigma value, was found to be 59 emuper gram. The coercive force was 241 oersteds, the squareness was 0.56.

One gram of this powder was mixed with 50 milliliters of a 7% solutionof cinnamic acid in isopropanol in a reactor known in the art as a Parrhydrogenator. This device was charged to a pressure of 50 psig at roomtemperature and was agitated with shaking for one hour. After this time,a two milliliter sample of the contents of the hydrogenator was takenand titrated with bromine solution until a stable color was achieved fora period of five minutes after the last addition of bromine. 83% of thecinnamic acid was found to have been hydrogenated.

EXAMPLE 24

The process described in Example 23 was repeated except 3.62 grams ofaluminum sulfate was substituted for the zinc nitrate used in theforegoing example. The resulting metal powder had a specific magneticmoment of 64 emu per gram and a coercive force of 225 oersteds and asquareness of 0.48. On the hydrogenation of cinnamic acid carried out inthe same method as described in the foregoing example, 66% of the acidwas hydrogenated.

EXAMPLE 25

A seed crystal was prepared by forming a first solution of 25 gramscobalt acetate tetrahydrate, 25 grams citric acid, 50 grams of Karosyrup and 50 grams of water and 50 grams of denatured ethanol. Thisfirst solution was added slowly and with stirring to a solution whichhad been preprepared and was formed of 25.2 grams oxalic acid dihydrate,150 grams ice, 150 grams denatured alcohol and 150 grams Karo. A verythick viscous suspension resulted. A quantity of 50 ml of thiscobalt-oxalate seed material was added to a 1-liter baffled Erlenmeyerflask which already contained a solution of 25 grams of oxalic aciddihydrate in 400 ml of water.

Next, a solution was prepared by dissolving 27.6 grams of nickel nitratehexahydrate in 150 ml of water. This solution was added slowly to theoxalic acid solution containing the suspended seed crystals. Vigorousagitation was maintained during the mixing procedure.

After the mixing was complete, the resulting suspension was filtered andthe crystals were washed with 500 ml of hot water and 250 ml of acetone.These crystals were dried and reduced in a tube furnace at 20% hydrogenand 80% nitrogen for four hours, in which time the CO₂ in the off-gaswas less than 0.02%. Then the tube furnace was cooled under 20%hydrogen-80% nitrogen mixture to room temperature. After the tube hadbeen purged with nitrogen and opened, the particles were covered withdry isopropanol.

The resulting material had a specific magnetic moment of 36 emu pergram, a coercivity of 175 oersteds, and a squareness of 0.4. One gram ofthe powder was mixed with 50 ml of a 7% solution of cinnamic acid inisopropanol in a Parr hydrogenator. The material was processed andtested as has been described in the other examples. 34% of the cinnamicacid had been reduced during the hydrogenation procedure.

It is of particular interest that the illustrated catalysts hadsubstantially constant activity at the time of their preparation and 29days thereafter. During the 29-day period they were stored underisopropanol but in an environment between about 75° F. and 105° F. thatwas over 90° F. during a large part of that time. Thus these catalystsfar outperform the Raney-type materials known in the art.

Dispersion--Strengthened Alloys

Another field of utility, not depending on ferromagnetic properties, yetadvantageously advanced by the process of the invention is that relatingto dispersion--strengthened alloys, e.g. those of the type described inNational Aeronautical and Space Administration (NASA) publicationSP5098. Thorium oxide, as other oxides, can be prepared by making athorium oxalate by the process described herein and converting theoxalate, to thorium oxide. Oxide so produced will derive a uniformity ofparticle size and morphology from the acicular oxalates and, apparentlyfor that reason are advantageous and economically useful in makingdispersion-strengthened alloys.

Others skilled in the metallurgical art and, indeed those skilled inother such metal-oxide-utilizing art including the pigment--making artwill recognize the value of the organmetallic salt-decomposing route foruse in manufacture of oxides for many purposes.

Testing Methods

Some of the materials illustrated by Specific Examples have been testedas set out below. The results are in Table 2. The following comments aremade on the various testing methods and parameters where such commentsare believed to be necessary or convenient.

A. Specific Magnetic Moment

The specific magnetic moment, or sigma value, is the value of thesaturation magnetic moment per unit, usually weight, of a magneticmaterial. It was measured on a vibrating sample magnetometer with a 4000oersted applied field. The instrument is calibrated directly inelectromagnetic units and is checked daily against a standard. Thevalues of sigma are given in electromagnetic units per gram of material.

B. Coercivity

The coercive force of the samples was measured at 25° C. in a 60 cycleBH loop tracer with an applied magnetic field of 3000 oersteds. Thevalues reported are in oersteds, magnetizing field strength at which theintrinsic flux density in the sample is zero when a sample of themagnetic material is in a symetrically cyclical magnetized condition. Inthe particles of the invention which are intended for magnetic tape, thecoercive force largely reflects size and shape of the metal particles.The higher coercive force belongs to the smaller particles or to themore acicular particles.

C. Coercive Force at Liquid Nitrogen Temperature

The chief reason for this measurement is to get a comparison betweencoercive force at room temperature and at very low temperature. If thecoercive force is controlled by shape anisotropy, there will be verylittle change in coercivity when the sample is cooled to liquid nitrogentemperature. If the coercive force is caused by crystalline anisotropy,the coercive force will change as the temperature to approximately thetenth power. This extremely large temperature coefficient makes it easyto detect materials whose coercive force is determined mainly bycrystalline anisotropy. Crystalline anisotropy materials are undesirablein the manufacture of magnetic tape because the settings for bias,record current, etc. have to be changed as a function of temperature.There have also been a number of other problems encountered in the artwith crystalline anisotropy-sensitive materials.

D. Squareness

Squareness of the BH loop is a measure of the remanent magnetizationdivided by the saturation magnetization. This is significant in magneticrecording particularly for long wavelength recording. Iron oxide has asquareness of 0.75 and is the currently used magnetic material for tape.Obviously the squareness ratio is a dimensionless number. These valuesare run on linseed oil emulsions of particles. The field causes theparticles to align magnetically with the field. The oil is viscousenough that the particles switch rather than rotate.

In this application, the oil-metal emulsion is placed in a 6-millimeterglass tube, then inserted into the sample oil of a 60-cycle loop tester.Squareness is measured at 2000 oersteds applied field. Values measuredthis way agree to two significant figures with the values measured inoriented tape in the direction of orientation.

E. Distribution of Switching Fields

This is a measure of the uniformity of coercive force within aparticulate sample. From data taken on the 60 cycle 5000 oersted BH looptester, then we can prepare a graph of the remanent flux as a functionof applied magnetic field. The slope of this curve, dφr/dH, defines thehistogram of number of particles switching as a function of appliedfield. This histogram then reflects the particle size and shape. As theparticle size gets smaller, the coercive force passes through a maximum.As the acicularity of the metal particles increases, the coercive forceincreases. So one can judge uniformity of size and shape from thismeasurement.

In actual practice, the metal particles are dispersed in a mixture of 10grams of Nujol mineral oil and 90 grams of paraffin. About 1 gram ofparticles is mixed, with random stirring in 3 grams of melted wax toform a stiff paste. This is then forced into a 6 mm glass tube andcooled to freeze it and immobilize the particles. φr is then measured asa function of the applied field from zero to 5000 oersteds. Formathematical expedience, data is taken at each 200 oersted increment,and a parabola is fitted through the first three data points, then theslope of the parabola is calculated at an even value of the field nearthe midpoint of the parabola. The smallest point is then dropped and thenext larger point is added. Then the parabola is again fitted and theslope is calculated. When all slopes are calculated, they are summed.Each slope is then divided by the sum of the slopes and the resultmultiplied by 100. This data is summarized on a table.

Salient features to look for are:

1. at low applied fields no particles should switch. This means no printthrough of recorded information from one layer of magnetic tape to thenext. Additionally, it means that there are no very large particlescapable of supporting more than one domain. Further, it means that thereare no very small particles, called superparamagnetic particles.

2. very little switching should place at fields higher than 3000oersteds. One should note, though, that during the dispersion to maketape, the high end of this curve "cleans up" and presents less of aproblem. The curve should be relatively sharply peaked, with the maximumvalue above 10%.

In general, the most advantageous ferromagnetic powders of the inventionare those wherein the peak switching is 10% or above but advantageously15% or higher, wherein less than 10% of the switching takes place at 50%of the peak switching field. All of the powders of Table D meet thesecriteria.

                  TABLE D                                                         ______________________________________                                        POWDER PROPERTIES                                                             DISTRIBUTION OF SWITCHING FIELDS                                              OF METAL POWDER IN PARAFFIN WAX, %                                            Field strength in                                                                          Example numbers                                                  oersteds     1        5        6       9                                      ______________________________________                                        0            0        0        0      0                                       200          1.08     .36      .36    .15                                     400          1.79     .37      .22    .46                                     600          10.04    1.82     1.17   2.15                                    800          18.42    5.89     5.13   4.19                                    1000         18.61    10.72    10.38  6.66                                    1200         14.63    14.63    14.89  10.84                                   1400         11.03    16.40    16.65  13.97                                   1600         9.08     14.83    15.15  14.28                                   1800         6.32     11.80    12.28  13.19                                   2000         3.92     8.34     9.12   11.09                                   2200         2.17     5.88     6.47   8.50                                    2400         1.14     4.33     4.20   6.71                                    2600         1.14     2.75     2.54   4.74                                    2800         .63      1.88     1.42   3.07                                    3000         0        0        0      0                                       ______________________________________                                    

The chemical stability of the ferromagnetic particles of the inventionis adequately measured by exposure to an environment of 50% relativehumidity at 165° F. for 100 hours. Some products of the invention willretain 70% or more of their magnetic moment (sigma value) after thistreatment. In addition to this chemical stability, the basicferromagnetic properties of a class of novel materials produced by theprocess of the invention are as follows:

Minimum squareness of 0.72

Minimum Sigma value of 110

Minimum Coercivity of 500

It is emphasized that these are properties defining a family of novelferromagnetic materials. In fact, substantially higher values can beachieved for each of these parameters as is specifically shown by thespecific examples. Moreover, there are many advantageous, perhaps novel,powders produced by the process described herein which are not withinthe above family of materials. Their failure to be included within thegroup defined by the above list of properties is not to be interpretedas a failure to recognize their novelty or an intent to exclude themfrom the scope of the invention defined the claims appended to thisspecification.

It is, of course, to be understood that the foregoing examples areintended to be illustrative and that numerous changes can be made in thereactants, proportions, and conditions set forth therein withoutdeparting from the spirit of the invention as defined in the appendedclaims.

What is claimed is:
 1. In a process for making acicular organometallicsalts of ferromagnetic metals the steps of reacting metal ions insolution with a carboxylic organic acid and precipitating anorganometallic salt, the improvement comprising the steps ofincorporating a metal-complexing agent in said solution to form at leastone soluble metal-complex compound, and initiating growth of saidorganometallic salt crystals in the presence of said metal complexcompound, said agent being incorporated in a quantity sufficient toenhance the acicular growth of said salt crystals.
 2. A process formaking small particles as defined in claim 1 wherein said solution is anaqueous medium comprising in addition to water, a water-soluble organiccompound which reduces the solubility of said organometallic salt in theliquid medium in which the salt is being formed.
 3. A process as definedin claim 1 wherein the solubility of organometallic salt in the solutionfrom which it is precipitated is less than 0.001 moles per liter.
 4. Aprocess as defined in claim 2 wherein the solubility of organometallicsalt in the solution from which it is precipitated is less than 0.001moles per liter.
 5. In a process as defined in claim 1 wherein saidorganometallic salt is a salt of a weak carboxylic acid.
 6. A process asdefined in claim 1 wherein said acid is oxalic acid.
 7. A process asdefined in claim 1 wherein said metallic portion of said organometallicsalt is predominantly selected from the group consisting of the metalsnickel, cobalt and iron or mixtures thereof, or mixtures comprising anyof said metals sufficient to render ferromagnetic the reduction productof said organometallic salts.
 8. A process as defined in claim 7 whereinsaid organometallic salt is a salt of a weak carboxylic acid.
 9. In aprocess for forming acicular, thermally-decomposable, organometallicsalt products of ferromagnetic metals by reacting a metal-bearing saltand a carboxylic acid, comprising the step of reacting saidmetal-bearing salt and said carboxylic acid in a liquid medium andprecipitating said organometallic salt from said medium, the improvementcomprising the steps of(a) initiating the precipitation by forming seedcrystals of a carboxylic acid and cations of a seed metal, said seedmetal being at least 50% by weight cobalt, said forming of seed crystalstaking place in the presence of a quantity of a complexing agent forsaid seed metal, said complexing agent forming means to facilitate apreferential crystal growth of said seed crystals along the long axisthereof; and (b) utilizing said seed crystals as growth initiating sitesfor formation of said acicular organometallic salt products or for seedcrystals subsequently used to form said organometallic salt products.10. A process as defined in claim 9 wherein said acicular organometallicsalt product is formed in the same medium as are said seed crystals. 11.A process as defined in claim 1 wherein said acicular organometallicsalt product is formed in a medium comprising substantially lesscomplexing agent than does said medium in which said seed crystals areformed.
 12. A process as defined in claim 9 wherein the metallic portionof said organometallic salt product is formed of atoms selected from thegroup of metals consisting of cobalt, iron and nickel, or mixturesthereof, and of any of said metals with other elements in quantitiessufficient to render ferromagnetic the reduction products of said saltproduct.
 13. A process as defined in claim 10 wherein the metallicportion of said organometallic salt product is formed of atoms selectedfrom the group of metals consisting of cobalt, iron and nickel, ormixtures thereof, and of any of said metals with other elements inquantities sufficient to render ferromagnetic the reduction products ofsaid salt product.
 14. A process as defined in claim 11 wherein themetallic portion of said organometallic salt product is formed of atomsselected from the group of metals consisting of cobalt, iron and nickel,or mixtures thereof, and of any of said metals with other elements inquantities sufficient to render ferromagnetic the reduction products ofsaid salt product.
 15. A process as defined in claim 9 wherein theacicular organometallic salt product is largely formed of particleshaving a length of at least about 0.5 micron and a length to diameterratio of at least about 8:1.
 16. A process as defined in claim 10wherein the acicular organometallic salt product is largely formed ofparticles having a length of at least about 0.5 micron and a length todiameter ratio of at least about 8:1.
 17. A process as defined in claim11 wherein the acicular organometallic salt product is largely formed ofparticles having a length of at least about 0.5 micron and a length todiameter ratio of at least about 8:1.
 18. A process as defined in claim12 wherein the acicular organometallic salt product is largely formed ofparticles having a length of at least about 0.5 micron and a length todiameter ratio of at least about 8:1.
 19. A process as defined in claim13 wherein the acicular organometallic product is largely formed ofparticles having a length of at least about 0.5 micron and a length todiameter ratio of at least about 8:1.
 20. A process as defined in claim14 wherein the acicular organometallic product is largely formed ofparticles having a length of at least about 0.5 micron and a length todiameter ratio of at least about 8:1.
 21. A process as defined in claim11 wherein said nickel comprises at least 8% of metal in saidorganometallic salt.
 22. A process as defined in claim 12 wherein saidnickel comprises at least 8% of metal in said organometallic salt.
 23. Aprocess as defined in claim 15 wherein said nickel comprises at least 8%of metal in said organometallic salt.
 24. A process as defined in claim9 wherein the complexing agent is selected from the group consistingof:ammonium salts or organic compounds selected from those bearing atleast two reactive groups selected from the group consisting ofhydroxyl, amino and carboxylic groups.
 25. A process as defined in claim10 wherein the complexing agent is selected from the group consistingof:ammonium salts of organic compounds selected from those bearing atleast two reactive groups selected from the group consisting ofhydroxyl, amino and carboxylic groups.
 26. A process as defined in claim11 wherein the complexing agent is selected from the group consisting ofammonium salts or organic compounds selected from those bearing at leasttwo reactive groups selected from the group consisting of hydroxyl,amino and carboxylic groups.
 27. A process as defined by claim 9 whereinsaid organometallic salt product is formed as an acicular fascescomprising numerous distinctive rod-like configurations of even greateracicularity.
 28. A process as defined in claim 9 wherein said liquidmedium comprises water and a water-soluble organic solvent, said solventproviding means to reduce the solubility of said organometallic saltproduct in said liquid medium.
 29. A process as defined in claim 10wherein said liquid medium comprises water and a water-soluble organicsolvent, said solvent providing means to reduce the solubility of saidorganometallic salt product in said liquid medium.
 30. A process asdefined in claim 11 wherein said liquid medium comprises water and awater-soluble organic solvent, said solvent providing means to reducethe solubility of said organometallic salt product in said liquidmedium.
 31. A process as defined in claim 12 wherein said liquid mediumcomprises water and a water-soluble organic solvent, said solventproviding means to reduce the solubility of said organometallic saltproduct in said liquid medium.
 32. A process as defined in claim 15wherein said liquid medium comprises water and a water-soluble organicsolvent, said solvent providing means to reduce the solubility of saidorganometallic salt product in said liquid medium.
 33. A process asdefined in claim 2 wherein said acid is oxalic acid.
 34. A process asdefined in claim 3 wherein said acid is oxalic acid.
 35. A process asdefined in claim 4 wherein said acid is oxalic acid.
 36. A process asdefined in claim 9 wherein the acid used to form said seed crystals isoxalic acid.
 37. A process as defined in claim 10 wherein the acid usedto form said seed crystals is oxalic acid.
 38. A process as defined inclaim 11 wherein the acid used to form said seed crystals is oxalicacid.
 39. A process as defined in claim 12 wherein the acid used to formsaid seed crystals is oxalic acid.
 40. A process as defined in claim 14wherein the acid used to form said seed crystals is oxalic acid.
 41. Aprocess as defined in claim 24 wherein the acid used to form said seedcrystals is oxalic acid.
 42. A process as defined in claim 25 whereinthe acid used to form said seed crystals is oxalic acid.